[0001] This invention relates to a method of sterilization and to a substance sterilized
by the method. It has general application, but particular application to packaging.
[0002] Derwent File Supplier No. AN 85-234441(JP60153982) appears to disclose the removal
of contamination compounds from the surfaces of articles by flowing water containing
dissolved ozone over the surfaces under the irradiation of UV. The water can contain
dissolved ozone or bubbles of ozonized gas.
[0003] Where the contamination compounds are organic compounds, they are partially oxidized
by the treatment, aldehydes, ketones and carboxylic acids being formed, and removed
by the water. Where the contamination compounds are inorganic compounds, they dissolve
or disperse in the water and are thus removed.
[0004] Ozone is decomposed under the irradiation of UV to form an oxygen radical, an hydroxyl
radical and a hydrogen peroxide radical. As such radicals have high activity but short
life-time, the treatment generates the radicals on the surfaces themselves and so
makes them most effective. The washing effect is further promoted because the reactivity
of the contamination compounds can be enhanced by the UV irradiation, thus breaking
down the compounds into smaller particles and into more hydrophilic compositions.
The washing effect was enhanced with increasing washing time and with increasing ozone
dissolved concentration. Use of oxygen gas in ozone generation increased the ozone
concentration and enhanced the washing effect.
[0005] Such treatment is concerned with removing contamination from the surface of articles
and is not concerned with sterilization in which micro-organisms are rendered non-viable.
[0006] US4309388 discloses sterilizing apparatus which comprises an enclosure surrounding
the top, bottom and sides of a central sterilizing enclosure space and adjacent inlet
and outlet enclosure spaces opening horizontally to the exterior of the enclosure
at the opposite ends thereof. A continuously moving conveyor carries open-topped glass
bottles to be sterilized horizontally through the inlet, sterilizing and outlet enclosure
spaces of the enclosure. The sterilizing enclosure space is divided by partition walls
into an upper compartment which opens at the bottom thereof into a lower compartment
immediately above the path of travel of the open tops of the bottles passing though
the lower compartment of the sterilizing enclosure space. Ozone-generating ultraviolet
lamps are mounted in the upper compartment and a blower circulates air between the
lower and upper compartments and through the opening of the upper compartment into
the lower compartment so that ozone generated in the upper compartment is directed
into the openings at the tops of the bottles moving in the lower compartment. Ozone
decomposition accelerating ultra-violet lamps are positioned in the inlet and outlet
enclosure spaces to accelerate decomposition of the ozone in the air escaping to the
surrounding atmosphere through the inlet and outlet enclosure spaces.
[0007] The UV employed for the purpose of indirectly sterilizing the bottles has a radiation
wavelength which is predominantly that in the wavelength band which generates ozone
and not in the wavelength band which kills micro-organisms. Although UV radiation
predominantly in the wavelength band which kills micro-organisms is employed, it is
not employed for the purpose of rendering the micro-organisms non-viable but simply
in order to degrade the ozone after its production.
[0008] CH387881 discloses a sterilization system in which the objects to be sterilized are
subjected in an enclosure to the simultaneous actions of (1) vapours of a bactericidal
substance, for example Methanogene, Trioxymethylene and Aldylene, (2) ozone generated
in the enclosure by a lamp radiating at a wavelength of 185 nm. and (3) UV radiation
of a wavelength of 253.7 nm.
[0009] In CH387881, the primary action of the ozone is particularly for the benefit of the
operator of the system, in that it deodorizes the vapours from the bactericidal substance
and removes their causticity from them, without however modifying their toxicity.
This primary action is accompanied by a secondary action in which the effect of the
ultraviolet radiation is to produce an activation of the bactericidal action, not
only of the ozone but also of the bactericidal vapours.
[0010] Patent Abstracts of Japan, Vol.12, No.22 (C-470) (2869) (JP 62-176595A) discloses
a method of decomposing a low molecular organic substance by adding ozonated water
to a mixture of hydrogen peroxide, and waste water containing the organic substance,
while the whole is irradiated with UV. It is not directed to the sterilization of
micro-organisms.
[0011] In US4366125, a long sheet material to be sterilized is passed through an atmosphere
of H
20
2 mist of low concentration and of droplet particle size of approximately 10 microns
at room temperature for approximately one second and is then irradiated for approximately
one second with UV lamps positioned to irradiate opposite surfaces of the sheet material,
whereby the material is sterilized as a result of the synergistic effect produced
by the combination of these two sterilization steps.
[0012] According to the present invention, there is provided a method of sterilization which
comprises subjecting micro-organisms to UV radiation predominantly in the wavelength
band which kills micro-organisms to render the micro-organisms non-viable, characterized
in that the micro-organisms are subjected to the UV radiation in the presence of ozone.
[0013] We have found that the use of UV in an ozone atmosphere instead of in air gives an
improved killing efficiency of micro-organisms. Moreover, we have not needed to employ
a bactericidal substance in addition to the ozone.
[0014] In the present specification, "ozone" means a gas comprised of significant amounts
of 0
3 radicals and hydroxyl radicals.
[0015] The ozone employed is preferably produced by subjecting air to a photoflux in the
vacuum ultraviolet range, which photons have between 8-10 ev and ionize only the oxygen
content, forming various activated oxygen compounds in the gas phase. Such activated
oxygen is advantageously PHOTOZONE (Registered Trade Mark) gas which is produced by
the PHOTOZONE (Registered Trade Mark) lamp obtainable from Water Management A/S of
Oslo, Norway.
[0016] Such activated oxygen has a relatively greater oxidation potential than ozone produced
by the classical method of employing a high voltage of between 8,000 and 10,000 volts
across electrodes, and thus a greater killing power of micro-organisms, owing to its
higher proportion of hydroxyl radicals.
[0017] The present invention is particularly useful for the sterilization of food contact
surfaces. Such surfaces can be the inside surfaces of walls, sheets, films, cups and
cartons. Where they are the inside surfaces of cartons ready to be filled, they may
be for example liquid contact surfaces of cartons formed from paperboard (or from
paperboard and aluminium foil, or from paperboard and polymer) with internal and external
plastics coatings. Such liquid can be long-life milk or orange juice, for example.
[0018] Tests in which the food contact surfaces of cartons were subjected to UV-C and were
contained in an ozone atmosphere appear to show a synergistic effect between the UV-C
and the ozone.
[0019] An important commercial advantage of the invention is that the required kill rates
of exposed micro-organisms are achieved by treatment times significantly less than
with known sterilization methods.
[0020] Tests in which the food contact surfaces of cartons were subjected not only to UV-C
in an ozone atmosphere but also to a pre-spray of H
20
2 appear to show additional synergism with consequential further improvement in treatment
times.
[0021] In order that the invention may be clearly understood and readily carried into effect,
examples of known sterilization treatments and of sterilization treatments according
to the invention will now be described.
EXAMPLES 1 - 7
[0022] These Examples set forth in Table I are a selection of various comparable tests and
illustrate the killing efficiency of exposure of
B. subtilis var. globigii (B-17) to UV-C (254 nm), 2% H
20
2, and/or heat, under various atmospheres. Air is mentioned at the commencement of
all Examples because it was the initial atmosphere and remained so unless and until
purged by the introduction of steam, or ozone, which latter remains the atmosphere
unless and until purged by steam.
[0023] The tests were performed in gable-top, aluminium-foil-lined cartons, not top-sealed.
The distance from the UV-C light source and the H
20
2 spray nozzle tip to the base of the cartons was a maximum of 28 cm.
[0024] Cartons were prior to the test inoculated with the spore suspension to a level of
approximately 10
6 spores per carton. Rinsing with plating was used to determine the spore load of the
carton.
[0025] After exposure to the various combinations of treatment, cartons were treated with
catalase to remove residual H
20
2. Cartons were then covered with nutrient agar on the inside and incubated for counting
survivors.
[0026] The conditions and exposure times for the tests are given in Table 1 together with
the results, the various treatments in each Example being given in their actual sequence.
TABLE I
EXAMPLE NO. |
TREATMENT |
INOCULUM |
DECIMAL REDUCTION |
1 |
Air + UV-C 254 nm (6s) |
5.9x105 |
4.0 |
2 |
Air + UV-C 254 nm (6s) |
6.3x104 |
3.4 |
3 |
Air + 2% H202 (150mg) + UV-C 254 nm (12s) |
3.9x106 |
<3.0 |
4 |
Air + 2% H202 (150mg) + UV-C 254nm (3s) + heat 150°C (2.6s) |
2.7x106 |
5.3 |
5 |
Air + 2% H202 (150mg) + UV-C 254nm (3s) + Steam (3s) |
3.0x106 |
5.2 |
6A |
Air + Ozone (31) [i.e. 3 litres] |
6.2x106 |
<1.0 |
6B |
Air + H20 (150mg) + Ozone (31) |
6.2x106 |
<1.0 |
6C |
Air + H20 (150mg) + Ozone (31) + UV-C 254nm (9s) |
6.2x106 |
4.4 |
6D |
Air + 2% H202 (150mg) + Ozone (31) + UV-C 254nm (9s) |
6.2x106 |
5.6 |
7A |
Air + Ozone (31) + UV-C 254nm (3s) + heat 150°C (2.6s) |
2.7x106 |
3.8 |
7B |
Air + 2% H202 (150mg) + Ozone (31) + UV-C 254nm (3s) + heat 150°C (2.6s) |
2.7x106 |
5.3 |
[0027] In each appropriate Example, the carton was flushed with Photozone, supplied at 0.8
l/s, for 5.0s.
[0028] Examples 6A to 6D illustrate the very great improvement obtained by the passage of
UV-C through a moist ozone atmosphere and the further improvement obtained by the
employment of an H
20
2 spray instead of a water spray. Examples 7A and 7B illustrate the great improvement
obtained by prior addition of H
20
2 compared with passing UV-C through a dry ozone atmosphere.
[0029] Examples 1 to 5 are illustrative of known treatments. Examples 6C, 6D, 7A and 7B
are illustrative of the present invention. The time periods given in each Example
are sequential rather than concurrent.
[0030] Testing was also carried out on the spores
Aspergillus niger as these are known to be highly resistant to ultraviolet radiation. These tests were
carried out in the form of a control to help justify previous results.
Spore Preparation
[0031] Aspergillus niger spores were inoculated on Malt extract agar and incubated at 25°C for one week.
[0032] Spores were harvested using a sterile loop and suspended in 1/4 strength Ringer's
solution with Tween 80 to achieve a concentration of approximately 10
5 - 10
6 spores/ml. Spores were applied to the surfaces by means of a cotton wool swab. Carton
surfaces were dried overnight followed by exposure to the sterilizing test conditions.
[0033] Bacillus subtilis var.globigii B17 spores were grown and isolated.
UV-C - Source
[0034] The UV-C source was IWASAKI irradiation equipment (254nm - UV-C) consisting of a
high-intensity sterilizer GHS 490145, nine lamp sets GHL 400-2 and three irradiator
sets GE 4301.
[0035] Ozone was produced by a Photozone lamp (185 nm - UV-C) from Water Management A/S.
Methods of Inoculation and Organisms
[0036] B.subtilis var. globigii (B17) are known to be highly resistant to hydrogen peroxide and ultra-violet radiation.
[0037] The method of producing a carton loading of 10
6 was as follows. A stock suspension of approximately 10
9/ml dilution was sprayed into the carton in 0.5 ml doses, where the residual in the
carton is approximately 10
6. The cartons were then dried overnight, and the verification of actual bacteriological
loading was carried out on 3/4 cartons. 9 ml of 0.25 strength Ringer's solution was
poured into the carton, the latter closed and shaken vigorously and approximately
20 seconds were allowed for the solution to collect into the base of the carton. 1
ml. was removed by pipette and further dilutions were carried out.
Spray System
[0038] It was decided to use a device already in use, which proved to give excellent coverage
on a 1 litre "Pure-Pak" carton. This device is commercially available from Metal Box
plc of Reading, Berkshire, United Kingdom.
Spray Parameters
[0039]
- Inlet air pressure
- = 90 psi. (6.4 kg/sq cm.)
- Atomising Air
- = 80 psi. (5.6 kg/sq cm.)
- Pulse air pressure
- = 60 psi. (4.2 kg/sq cm.)
- Tank pressure
- = 20 psi. (1.5 kg/sq cm.)
- Discharge air pressure
- = 10 psi. (1.05 kg/sq cm.)
- Nozzle tip to carton base
- = 270 - 280 mm.
[0040] This setting remained standard throughout all of the testing where spraying of H
20
2 was required. The only change was to the duration of the spraying time, which was
varied to give differing levels of H
20
2 within the carton.
1. A method of sterilization which comprises subjecting micro-organisms to UV radiation
predominantly in the wavelength band which kills micro-organisms in order to render
the micro-organisms non-viable, characterized in that the micro-organisms are subjected
to the UV radiation in the presence of ozone.
2. A method according to claim 1, in which said wavelength band is between 220 and 330
nanometres.
3. A method according to claim 1 or 2, wherein the micro-organisms are subjected to UV
radiation as aforesaid in the presence also of moisture.
4. A method according to claim 3, wherein said moisture is provided by a spray of water
or by steam.
5. A method according to any preceding claim, wherein said micro-organisms are subjected
to UV radiation as aforesaid while at a surface of a packaging material.
6. A method according to any preceding claim, and further comprising subjecting said
micro-organisms to UV radiation as aforesaid in the presence also of hydrogen peroxide.
7. A method according to any preceding claim, and further comprising subjecting said
micro-organisms to UV radiation as aforesaid in the presence of a low concentration
of hydrogen peroxide so as to obtain a synergistic effect between the UV radiation
and the hydrogen peroxide in rendering the micro-organisms non-viable.
8. A method according to any preceding claim, wherein the subjecting of the micro-organisms
to the UV radiation as aforesaid obtains a synergistic effect between the UV radiation
and the ozone insofar as the rendering of the micro-organisms non-viable is concerned.